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14 BEAet�.11_ �.�/3 <br />Vol k�TT-L�ie�JAN <br />G.9NE LoD.Z Gfl• Z9 <br />�"vAJE 8$ <br />Nem" of supplier. Gwner a Dealer <br />Ad&*$$ Ne. and Street IS) <br />71 <br />City State <br />Det. of last <br />15. TANK TO TEST <br />15a. BRIEF DIAGRAM OF TANK FIELD <br />' <br />16. CAPACITY <br />``°rat <br />Sutton Chart <br />d ( <br />;. <br />S%` <br />A7-fAGM5Nominal <br />Bottom of tank to grade' <br />Capacity <br />a Tank Manufacturer's Chaff <br />Identay by positionLYd <br />Q /A&)?./ <br />30 tn. <br />Gallons <br />❑Company Engineering Gore <br />L/ <br />. 1 <br />Tolsl quantity in Reciprocal <br />/ <br />1—�j Charts supplied with <br />I/} <br />2 Height to 12" mark from bottom of tank/S <br />By most accurate <br />I /10J Z—JQ <br />❑Omer <br />Brand and Grade <br />capacity chart available <br />Galton <br />In. <br />17. FILL -UP FOR TEST <br />P <br />Stick Water BonOm . Inventory <br />before Fm -up �• <br />• to A' - - . Oailona.. Tank Diameter <br />18. SPECIAL CONDITIONS AND PROCEDURES TO TEST THIS TANK BWaterinlank Y'�` Uriels)betogtestedwithLVLLT <br />Sea manual sections applicable. Check below and record <br />procedure In loo (24 <br />^t_'YNigh water table In lank excavation <br />Type of Product ........................................ <br />List maximumavowable test pressure lot all testa. <br />Hydrometer Employed <br />19. TANK MEASUREMENTS FOR <br />Temperature In Tank <br />Four pound rule does not spay to doublewaoed links. <br />' <br />?STT ASSEMBLY <br />/��• <br />Temperature of Sample ................................. 1fLltl_Sr_ 'F <br />Complete section below: - <br />•, <br />• <br />Bottom of tank to grade' <br />136 <br />- <br />l <br />Add 30' for "T' probe easy ........................... <br />30 tn. <br />I Is four pound rule tequired? <br />(� <br />Yet DO No ❑ <br />Total tubing to assemble — approximate ............. <br />�"' "T In. <br />Tolsl quantity in Reciprocal <br />Volume Mange In <br />' <br />•] <br />t <br />20. EXTENSION NOSE SETTING <br />2 Height to 12" mark from bottom of tank/S <br />In. <br />/ <br />Tank top to grade' .................................. <br />In. <br />®R <br />V "' P.S.L <br />Extend hose on auction tuba It' or more <br />Z y <br />J. pressure at bottom of tank <br />lank lop ...................................... <br />In <br />Jbelow <br />r ' 6 + <br />'It FRO pipe extends above grade, use top of IIIL <br />1, Pressure at top of lank <br />P.S.I. <br />>Y <br />of burial <br />Its. <br />table <br />NOTES:. <br />The above calculations are to be used for dry soft conditions lei <br />establish a positive pressure advantage, or when using the four pound <br />ruts to Compensate for the presence of subsurface waist In the lank <br />area. <br />Oster to N.F.P.A. 30. Seaton$ 2-3.2.4 end 2-7.2 and the tank <br />manufacturer regarding agowabie System lee/ pressurfs. <br />22. Therm I.Senior reading alter circulation <br />digits <br />781 7 0 IF <br />Be�lw/germy <br />23. Digits per IF in range of expected Change Vii.--- <br />dighs <br />COEFFICIENT OF EXPANSION (Complete alter circulation) <br />24a, orrected A.P.I. Gravity <br />bsamod A.P.. revity................................... <br />Total Gallon$ - <br />Galtona as. nesding r <br />1/(132.9 <br />Tor (p Ff 2-0 <br />— <br />WA -e' <br />Transfer total to line 254 <br />21. VAPOR RECOVERY SYSTEM ®ewe t CR stage if <br />24b. COEFFICIENT OF EXPANSION <br />RECIPROCAL METHOD <br />' <br />Type of Product ........................................ <br />! <br />Hydrometer Employed <br />H <br />Temperature In Tank <br />7J <br />After Circulation ..................................-...... <br />r• •F <br />/��• <br />Temperature of Sample ................................. 1fLltl_Sr_ 'F <br />— / .F <br />Difference I-/-) ......................................... <br />Observed A.P.I. <br />/Gravity <br />y.................................. <br />Page a 6 b <br />Reciprocal <br />Tolsl quantity in Reciprocal <br />Volume Mange In <br />full tank 116 or IT) <br />this lank per IF <br />- Transfer to line Zea. <br />Hydrometer employed .... N <br />24c. FORT STIP NG WITH WATER ase TsDle C a O <br />Observed Sample Temperature •F �\ <br />Cerretted A.P.I. Gravity waist Tsmperatura altar Circulareo•F. From Table A ......................... Table C ........... .... ........... •F <br />Coefficient of Expansion Coefficient of Water <br />for Involved Product Table 0 ................................................ <br />From Table 13............................................�� <br />Transfer COE to fins 250. Added Sufficient? 1:1 Yet ❑ No Transfer COE to line 25b. <br />25. (a) at (b) U gallons <br />Total quantity M Coelnclenl of expansion for Volume Change In IMS lank <br />hull Isnk Its or 17) involved product per IF <br />26. (a) > 97.3755 3/ 9 , oz- y99t� Thio is z- <br />Volume change per If (25 or 24b) Oighs per IF to lest VOluma change Per digit tmH <br />nano. (29) Cuntpute ro a dattn,al pf.c$$. factor (al <br />